WO2012099172A1

WO2012099172A1 - Method for producing fatty acid ester

Info

Publication number: WO2012099172A1
Application number: PCT/JP2012/050975
Authority: WO
Inventors: 鈴木　茂雄
Original assignee: 味の素株式会社
Priority date: 2011-01-18
Filing date: 2012-01-18
Publication date: 2012-07-26
Also published as: JP5924268B2; US20130302864A1; JPWO2012099172A1

Abstract

A method for producing a fatty acid ester, characterized in that a culture obtained by culturing microalgae in a culture medium is made to react at a medium temperature and subsequently alcohol is added for a reaction at a lower temperature than the medium temperature, and a fatty acid ester is collected from the resulting reaction product.

Description

Production method of fatty acid ester

The present invention relates to a method for producing a fatty acid ester using algae. Fatty acid esters are used in various fields such as food additives, chemical products, cosmetics, and pharmaceuticals.

Fatty acid esters are industrially produced from animals, plants, fish, and oils and fats derived from waste oil by transesterification. As these transesterification reactions, methods utilizing a catalyst such as acid, alkali, metals, or lipase are known. For example, the methods described in Non-Patent Documents 1 to 4 can be mentioned. On the other hand, a supercritical method is used in addition to a method using a catalyst. For example, the methods described in Non-Patent Documents 5 to 7 can be mentioned.

In the industrial production of fatty acid esters by transesterification, fish oil, animal oil, vegetable oil, waste liquid oil, etc. are used as fats and oils. As fats and oils used in the production method by transesterification of fatty acid esters, oils and fats derived from higher plants such as soybean and palm palm are often used. These are fats and oils that can be easily obtained from seeds by pressing or solvent extraction. On the other hand, the fats and oils contained in microalgae have a content comparable to that of soybeans and palm oil seeds per dry weight, but the dry alga body weight per algal culture is less than 1%. The process of separating the alga bodies, dehydrating them, crushing the cells, taking out the fats and oils, and further purifying them is complicated and difficult. It is possible to produce fatty acid esters from fats and oils purified from algae using acid, alkali or lipase (Patent Document 1, Non-Patent Documents 8 to 9). Further, in Patent Documents 2 to 4, alcohol is added to microalgae and the fats and oils are directly transesterified in the cells, but both methods require an acid or an alkali catalyst for the transesterification reaction.

Synechocystis, which is a typical recombinable algae, can produce a large amount of fatty acids by expressing acetyl-CoA carboxylase and thioesterase (Non-patent Document 10), and by expressing diacylglycerol acetyltransferase. It is known to produce triglycerides (Patent Document 5). Therefore, it is easy to produce fatty acid esters from Synecocystis fats and oils using a catalyst such as acid, alkali or lipase. In addition, it is known that Synechocystis can express pyruvate decarboxylase and alcohol dehydrogenase, produce ethanol, and produce fatty acid esters in cells by ethanol acetyltransferase (Patent Document 6). Without the method, a method for producing fatty acid esters from fats and oils in algal cells is not known.

Generally, algae use lipase to decompose lipids and fats in cell membranes (Non-patent Document 11). In diatoms, it has been confirmed that lipase activity increases due to starvation of silica and that fats and oils are decomposed into fatty acids (Non-Patent Document 12), but it is possible to produce fatty acid esters in algal cells by adding alcohols to them. There is no report so far.

Further, it has been known that cells are crushed and organic substances are extracted by treating chlorella at high temperature (Patent Documents 7, 8, and 9), but there is no report that directly converts intracellular fats and oils into fatty acid esters. In addition, it has been known that low-molecular-weight nucleic acid-related substances increase by maintaining chlorella at 40 to 55 ° C. and self-digesting (Patent Document 10). Never before.

International Publication No. 2010/000416 US Patent Application Publication No. 20080241902 Chinese Patent Application No. 1015580857 US Patent Application Publication No. 20090158638 US Patent Application Publication No. 2011081178 International Publication No. 2010/011754 JP-A-9-75094 International Publication No. 2006/095964 US Patent Application Publication No. 20070202582 JP 62-278777 A

The present invention provides a more efficient method for producing a fatty acid ester, in particular, an acid or alkali catalyst that has been conventionally used mainly with fats and oils derived from animals, plants, fish and waste liquids as substrates. The present invention provides a cheaper fatty acid ester production method that does not require addition of a catalyst to the fatty acid ester production method.

As a result of intensive studies to solve the above-mentioned problems, the present inventors reacted algal culture at an intermediate temperature before reacting with alcohol, thereby adding algal cells without adding acid or alkali. And found that fatty acid esters can be produced efficiently. Based on this finding, the present invention has been completed.
(1) (a) reacting a culture obtained by culturing microalgae in a medium at medium temperature;
(B) Then, an alcohol is added and reacted at a temperature lower than the intermediate temperature,
(C) A method for producing a fatty acid ester, wherein the fatty acid ester is collected from the reaction product obtained.
(2) The method as described above, wherein the temperature of the reaction (a) is 40 ° C. or higher.
(3) The method as described above, wherein the temperature of the reaction (a) is 70 ° C or lower.
(4) The method as described above, wherein the pH of the reaction (a) is from weakly acidic to weakly alkaline.
(5) The method as described above, wherein the temperature of the reaction of (b) is 5 ° C or higher.
(6) The method as described above, wherein the temperature of the reaction (b) is 60 ° C. or lower.
(7) The method as described above, wherein the alcohol concentration in the reaction (b) is 5% or more.
(8) The method as described above, wherein the alcohol concentration in the reaction (b) is 70% or less.
(9) The method as described above, wherein the alcohol added to the reaction (b) is a lower alcohol having 5 or less carbon atoms.
(10) The method as described above, wherein the alcohol added to the reaction (b) is a higher alcohol having 6 or more carbon atoms.
(11) The method as described above, wherein the fatty acid ester is extracted by further treating with an organic solvent after the two-step reaction of (a) and (b), and the fatty acid ester is collected from the extract.
(12) The method according to the above, wherein the precipitate separated by centrifugation after the two-stage reaction is treated with an organic solvent.
(13) The organic solvent treatment is performed with methanol, ethanol, 2-propanol, acetone, butanol, pentanol, hexanol, heptanol, octanol, chloroform, methyl acetate, ethyl acetate, dimethyl ether, diethyl ether, or hexane. A method as described above, characterized.
(14) The method as described above, wherein the microalgae are algae belonging to the green plant phylum.
(15) The method according to the above, wherein the microalgae is an algae belonging to a green alga, a treboxya algae, or a platino alga steel.
(16) The method according to the above, wherein the microalgae are algae belonging to the green alga class.

The fatty acid ester can be efficiently produced by using the present invention.

Examination of temperature conditions of first stage reaction in two stage reaction of algae culture Examination of time of first stage reaction in two stage reaction of algae culture Examination of pH of first stage reaction in two stage reaction of algae culture Examination of methanol addition concentration in second stage reaction in two stage reaction of algae culture Examination of the second stage reaction time in the two stage reaction of algae culture Examination of temperature of second stage reaction in two stage reaction of algae culture Examination of added alcohol in second-stage reaction in two-stage reaction of algae culture Qualitative properties of fatty acid alcohol esters produced by two-step reaction of algae cultures Results of a two-step reaction with Scenedesmus abundans UTEX 1358

Hereinafter, the present invention will be described in detail.
<1> Microalgae used in the present invention and its culture method Any microalgae can be used in the present invention, but it is a microalgae that accumulates starch and / or fats and oils in the algae. It is preferable.

Algae refers to all organisms that perform oxygen-generating photosynthesis, excluding moss plants, fern plants, and seed plants that inhabit the ground. Algae includes prokaryotes, cyanobacteria, eukaryotes, gray plant gate (Glaucophyta), red plant gate (Rhodophyta), green plant gate (Chlorophyta), cryptophyte Gates (Cryptophyta), Haptophyta (Haptophyta), Heterokontophyta, Dinophyta, Euglenophyta, Euglenaphyta Included are various unicellular and multicellular organisms that are classified as Chlorarachniophyta. Microalgae refers to algae with a microscopic structure excluding seaweeds that are multicellular organisms from these algae (Biodiversity Series (3) Diversity and strains of algae: edited by Mitsuo Senbara 1999)).

Plants including microalgae are known to accumulate oils and fats as storage substances (Chisti, Y. 2007. Biotechnol Adv. 25: 294-306). As such algae, those belonging to the green plant gates and the unequal hairy plant gates are well known. Among the green plant gates, there are algae belonging to the Chlorophyceae, and the algae belonging to the Chlorophyceae are Chlorella minutissima (Bhatnagar A, 2010 Appl Biochem Biotechnol. 161: 523-36) Senedesmus・ Scenedesmus obliquus (Shovon, M. et al. 2009. Appl Microbiol Biotechnol. 84: 281-91) Neochloris oleoabundans (Tornabene, TG et al. 1983. Enzyme and Microb. Technol. 5: 435-440) Nanonochloris sp. (Takagi, M. et al. 2000. Appl. Microbiol. Biotechnol. 54: 112-117). There are golden algae (Chrysophyceae), Dictyochophyceae, Pelagophyceae, Rhaphidophyceae, Diatomae (Bacillariophyceae), Brown algae (Phaeophyceae), yellow green algae Class Xanthophyceae and Eustigmatophyceae are classified, but as algae belonging to the commonly used diatom class, Thalassiosira pseudonana (Tonon, T et al. 2002. Phytochemistry 61: 15 -24). Specifically, as Chlorella minutissima, Chlorella minutissima UTEX 2314, Senedesmus oblicus, specifically as Scenedesmus obliquus UTEX393, Neochloris oleo abundance, specifically Neochloris oleoabundans UTEX 1185, Nanochloris Examples of SP include Nannochloris sp. UTEX LB 1999 strain, and examples of Thalassiosira sudonana include Thalassiosira pseudonana UTEX LB FD2. These strains can be obtained from The University of Texas at Austin, The Culture Collection of Algae (UTEX), 1 University Station A6700, Austin, TX 78712-0183, USA.
Further, EPA / DHA-producing algae, which are high-functional fatty acids, are well known that belong to the green plant gate, the alien hair plant gate, the red plant gate, or the hapto plant gate. Among the green plant gates, there are algae belonging to the class of green algae, Plasinophyta, and Trevoxia algae, and the well-known algae belonging to the class of green algae Chlorella minutissima (Rema, V et al. 1998. (JAOCS. 75: 393-397) Examples of the alien phytophytes include algae belonging to the diatom class (Bacillariophyceae) and the true eye-point algae class (Eustigmatophyceae). Thalassiosira pseudonana (Tonon, T et al. 2002. Phytochemistry 61: 15-24), Eustigmatophyceae includes the nanochloropsis oculata.

There is a lot of knowledge about the culture of microalgae, and Chlorella, Arthrospira (Spirulina), Dunaliella salina, etc. are edible on a large scale industrial culture (Spolaore, P. et al. 2006. J. Biosci. Bioeng. 101: 87-96). For example, 0.3 × HSM medium (Oyama, Y. et al. 2006. Planta 224: 646-654) can be used for Chlamydomonas reinhardi, and 0.2 × Gumborg medium (Izumo, A. et al. 2007. Plant Science 172: 1138-1147) can be used. For Chlorella vulgaris, BG-11 medium or M8 medium (Ramkumar, K.M et al. 1998. Biotech. Bioeng. 59: 605-611) can be used. Neochloris Oreo abundance and Nanochloris SP are modified NORO medium (Yamaberi, K. et al. 1998. J. Mar. Biotechnol. 6: 44-48; .54: 112-117) and Bold's Basal Medium (Tornabene, T. G. et al. 1983. Enzyme and Microb. Technol. 5: 435-440; Archibald, P. A. and Bold, H. C. 1970. Phytomorphology (20: 383-389) and Daigo IMK medium (Ota, M. et al. 2009. Bioresource Technology. 100: 5237-5242). As for the algae belonging to the diatom class, F / 2 medium (Lie, C.-P. and Lin, L.-P. 2001. Bot. Bull. Acad. Sin. 42: 207-214) Etc. can be used suitably. A photobioreactor can also be used for culturing microalgae (WO2003 / 094598 pamphlet).

In many cases, 1-50% of the preculture solution is added to the volume of the main culture. The initial pH is preferably around 7-9 neutral, and pH adjustment is often not performed during culturing, but it may be done as needed. The culture temperature is preferably 25-35 ° C., and particularly around 28 ° C. is a commonly used temperature, but the culture temperature may be any temperature suitable for the algae used. In many cases, air is blown into the culture medium, and an aeration rate of 0.1-2 vvm (volume per volume per minute) per one minute of the culture solution volume is often used as the aeration rate. Further, CO ₂ is blown in order to accelerate the growth, but it is preferable to blow about 0.5-5% with respect to the aeration amount. The optimal intensity of light irradiation varies depending on the type of microalgae, but about 1,000-30,000 lux is often used. As a light source, a white fluorescent lamp is generally used indoors, but is not limited thereto. It is also possible to incubate outdoors with sunlight. If necessary, the culture solution may be stirred or circulated with an appropriate strength. Algae are known to accumulate fats and oils in the algae when the nitrogen source is depleted (Thompson GA Jr. 1996. Biochim. Biophys. Acta 1302: 17-45), which limits the concentration of the nitrogen source. The medium can also be used for the main culture.

In the present invention, the culture of microalgae includes a culture solution containing algal bodies and algal bodies recovered from the culture solution.

The method for recovering the algal cells from the culture solution is possible by general centrifugation, filtration, or sedimentation by gravity using a flocculant (Grima, E. M. et al. 2003). Biotechnol. Advances 20: 491-515).

Particularly in the present invention, it is preferable to concentrate microalgae by centrifugation or the like before the reaction at medium temperature. For concentration of algal bodies, the solution components are removed, and the concentration per unit solution of the dry weight of microalgae is 25 g / L or more, preferably 250 g / L or more (separated from the medium by a method such as centrifugation). Including suspending the algal bodies in a liquid to a desired concentration) and precipitating and separating the algal bodies from the medium.

<2> Reaction method and reaction product of microalgae culture of the present invention In the present invention, the microalgae culture is subjected to a two-stage reaction at a medium temperature and a medium to low temperature (a temperature lower than the medium temperature) after addition of alcohol. (Ie, subjected to a two-step reaction), and the processed microalgae (reactant) is used to collect fatty acid esters.

In the present invention, the reaction product of microalgae means a reaction solution obtained by subjecting a culture of microalgae to a two-stage reaction at a medium temperature and a medium to low temperature after addition of alcohol. The treated product may be subjected to further extraction or fractionation and / or another treatment from the reaction solution subjected to the two-stage reaction as long as subsequent collection of the fatty acid ester is not prevented. In the treated product of the present invention, by-products are produced in addition to fatty acid esters. Among them, glycerol produced by transesterification of fats and oils is L-amino acid produced by bacteria having L-amino acid producing ability and chemical products. You may use it.

The second stage reaction of the two stage reaction is a reaction that produces a fatty acid ester. The first-stage reaction is a reaction that changes the state of the microalgae culture so as to promote the formation reaction of the second-stage fatty acid ester.
In the present invention, the temperature in the two-stage reaction may be a temperature sufficient to increase the fatty acid ester in the reaction product after the medium temperature reaction and the medium to low temperature reaction after addition of the alcohol, and after the first stage reaction, Lower the temperature and perform the second stage reaction. Here, the lower limit of the temperature of the first stage reaction is usually 40 ° C. or higher, preferably 45 ° C. or higher, more preferably 50 ° C. or higher, and the upper limit is usually 70 ° C. or lower, preferably 65 ° C. or lower, More preferably, it is 60 ° C. or lower. The lower limit of the temperature of the second-stage reaction is usually 5 ° C or higher, preferably 20 ° C or higher, more preferably 30 ° C or higher, and the upper limit is usually 60 ° C or lower, preferably 50 ° C or lower, more preferably Is 45 ° C or lower.

In the present invention, the first-stage reaction in the two-stage reaction may be performed by reacting the culture obtained by the above-described algal culture method as it is, but may be used after being concentrated as described above. For example, the alga bodies that have been once centrifuged and then precipitated may be used as the reactant.

Further, the pH during the reaction may be adjusted to weakly acidic or weakly alkaline before the first stage reaction.

Here, the pH of weak acid is preferably 3.0 to 6.5, more preferably 4.0 to 6.0. Further, the pH of the weak alkali is preferably 7.5 to 12.0, more preferably 9.0 to 11.0.

As a method of adding alcohol before the second stage reaction, alcohol may be added to the reaction liquid of the first stage reaction, or after removing the liquid phase of the reaction liquid of the first stage reaction by centrifugation or the like. A reaction solution for the eye reaction may be added.

The concentration of the alcohol added before the second stage reaction is preferably at least 5% or more, preferably 10% or more, more preferably 20% or more. The upper limit is usually 70% or less, preferably 60%, more preferably 50% or less.

The alcohol to be added is a lower alcohol having 5 or less carbon atoms such as methanol, ethanol, propanol, isopropanol, butanol, pentanol, ethylene glycol, or hexanol, heptanol, octanol, nonanol, decanol, undecanol, dodecanol, tridecanol, tetradecanol, and the like. Higher alcohols having 6 or more carbon atoms such as knoll may be used.

In the present invention, the first-stage reaction (treatment at intermediate temperature) is preferably performed for at least 5 minutes or more, preferably 10 minutes or more, more preferably 20 minutes or more. The first stage reaction is usually 120 minutes or less, more preferably 60 minutes or less. Further, the second-stage reaction (treatment at medium and low temperatures) has a lower limit of at least 10 minutes, preferably 30 minutes or more, more preferably 120 minutes or more, and an upper limit of usually 15 hours or less, preferably It is preferably 10 hours or less, more preferably 5 hours or less.

As a method for extracting a fatty acid ester from a reaction product after the two-step reaction, a method for extracting fats and oils from general algae can be applied. For example, organic solvent treatment, ultrasonic treatment, bead crushing treatment, acid treatment, alkali treatment There are methods such as treatment, enzyme treatment, hydrothermal treatment, supercritical treatment, microwave treatment, electromagnetic field treatment, or pressing treatment. It is preferable that the fatty acid ester is eluted extracellularly and the fatty acid ester is collected from the eluate.

In the present invention, the organic solvent treatment after the two-step reaction is methanol, ethanol, 2-propanol, acetone, butanol, pentanol, hexanol, heptanol, octanol, chloroform, methyl acetate, ethyl acetate, dimethyl ether, diethyl ether, hexane, etc. Is mentioned.

After the two-stage reaction, the reaction solution is preferably separated into a precipitate and a supernatant by centrifugation. Further, after the two-step reaction, an organic solvent may be added, and an extraction method using two layers of an aqueous layer and an organic solvent layer may be used.

In the present invention, the reason why the addition of the catalyst is not required is that the lipase in the cells of microalgae is likely to act on the lipid by the first-stage reaction, and by the lipase, fat, ceramide (Ceramide), phospholipid soot ( This is probably because Phospholipid) and Glycolipid are transesterified with externally added alcohol.

Generally, transesterification with lipase is promoted by the addition of an organic solvent other than alcohols. Accordingly, an organic solvent in an amount effective for promoting the reaction in the second stage reaction may be added. Examples of such organic solvents include hexane, heptane, isooctane chloroform, ethyl acetate, petroleum ether, and the like.

Hereinafter, the present invention will be described in more detail with reference to examples. In this example, Chlorella kessleri 株 11h strain obtained from University of Texas Algae Culture Collection (The University of Texas at Austin, The Culture Collection of Algae (UTEX), 1 University Station A6700, Austin, TX 78712-0183, USA) ( UTEX 263) and Scenedesmus abundans UTEX 1358 strain were used.

<Example 1> Culture of microalgae Chlorella kessleri 11h strain Chlorella kessleri 11h strain at 30 ° C in a 1000 mL medium bottle containing 800 mL of 0.2 x Gamborg B5 medium (Nippon Pharmaceutical), light intensity 7,000 lux (manufactured by TOMY) Culturing apparatus CL-301) was cultured for 7 days while blowing a mixed gas of air and 3% CO ₂ at 400 mL / min, and this was used as a preculture solution. Note that white light from a fluorescent lamp was used as the light source. 0.2 × Gambog B5 Add 800 mL of preculture to a 1000 mL medium bottle containing 800 mL of medium, and mix air and 3% CO ₂ at 400 mL / min at a culture temperature of 30 ° C and light intensity of 7,000 lux. The culture was carried out for 14 days while blowing.

(0.2 x Gamborg B5 medium)
KNO ₃ 500 mg / L
MgSO ₄・ 7H ₂ O 50 mg / L
NaH ₂ PO ₄・ H ₂ O 30 mg / L
CaCl ₂・ 2H ₂ O 30 mg / L
(NH ₄ ) ₂ SO ₄ 26.8 mg / L
Na ₂ -EDTA 7.46 mg / L
FeSO ₄・ 7H ₂ O 5.56 mg / L
MnSO ₄・ H ₂ O 2 mg / L
H ₃ BO ₃ 0.6 mg / L
ZnSO ₄・ 7H ₂ O 0.4 mg / L
KI 0.15 mg / L
Na ₂ MoO ₂・ 2H ₂ O 0.05 mg / L
CuSO ₄・ 5H ₂ O 0.005 mg / L
CoCl ₂・ 6H ₂ O 0.005 mg / L
120 ℃ 15 minutes Autoclave sterilization

<Example 2> Examination of the temperature conditions of the first-stage reaction in the two-stage reaction of algae The culture solution obtained in Example 1 was centrifuged, and sterilized water was added to the precipitate to prepare a 1-fold suspension. . After adjusting the pH of the suspension to 4.5 with 1N HCl solution, 1 ml was placed in a 1.5 ml Eppendorf tube and pre-incubated for 10 minutes at 45 ° C., 50 ° C., 55 ° C., and 60 ° C. at rest. Next, after incubating each sample at 1000 rpm for 30 minutes at the same temperature as above, each sample was centrifuged, and 200 μl of a 10% methanol solution was added to the precipitate. Each sample was incubated at 42 ° C. and 1000 rpm for 5 hours, and an ester exchange reaction between oil and methanol was performed. Lipids were extracted from the obtained samples, and fatty acid methyl esters were measured. The measurement results are shown in FIG. After induction at 45 ° C. for 30 minutes, almost no formation of fatty acid methyl ester was confirmed at 42 ° C. for 5 hours, but after induction treatment at 50 ° C. or higher for 30 minutes, formation of fatty acid methyl ester was confirmed at 42 ° C. for 5 hours, The yield increased most at an induction temperature of 55 ° C.

<Example 3> Examination of the time of the first stage reaction in the two-stage reaction of algae The culture solution obtained in Example 1 was centrifuged, and sterilized water was added to the precipitate to prepare a 1-fold suspension. After adjusting the pH of the suspension to 4.5 with 1N HCl solution, put 1 ml in a 1.5 ml Eppendorf tube, preincubate for 10 min at 55 ° C, then 55 ° C, 1000 rpm, 10 min, 20 min, 30 min, 40 min, After incubation for 50 min or 60 min, each sample was centrifuged and 200 μl of 10% methanol solution was added to the precipitate. Each sample was incubated at 42 ° C. and 1000 rpm for 5 hours, and an ester exchange reaction between oil and methanol was performed. Lipids were extracted from the obtained samples, and fatty acid methyl esters were measured. The measurement results are shown in FIG. The yield of fatty acid methyl ester production increased at 55 ° C for 20 min compared to the induction temperature of 55 ° C for 10 min. On the other hand, at 55 ° C. and induction temperature after 30 min, the yield tended to decrease as the induction time increased.

<Example 4> Examination of pH of first-stage reaction in two-stage reaction of algae The culture solution obtained in Example 1 was centrifuged, sterilized water was added to the precipitate, and a 1-fold suspension was prepared. The suspension was adjusted to each pH with 1N HCl solution or 1N NaOH, then 1 ml was put into a 1.5 ml Eppendorf tube, pre-incubated for 5 min at 55 ° C., then incubated at 55 ° C., 1000 rpm, 20 min. Samples were centrifuged and 200 μl of 10% methanol solution was added to the precipitates. Each sample was incubated at 42 ° C. and 1000 rpm for 5 hours, and an ester exchange reaction between oil and methanol was performed. Lipids were extracted from the obtained samples, and fatty acid methyl esters were measured. The measurement results are shown in FIG. Production of fatty acid methyl esters was confirmed in the pH range of 3.0 to 10.5, and high yields were shown under two conditions, pH 4.5 in the weakly acidic region and pH 10.5 in the weakly alkaline region.

<Example 5> Examination of methanol addition concentration in two-stage reaction of algae The culture solution obtained in Example 1 was centrifuged, and sterilized water was added to the precipitate to prepare a 1-fold suspension. Adjust the pH of the suspension to 4.5 with 1N HCl solution, add 1 ml to a 1.5 ml Eppendorf tube, preincubate at 55 ° C for 5 min, incubate at 55 ° C, 1000 rpm, 20 min, then centrifuge. 200 μl of 5-50% methanol solution was added to the precipitate. Each sample was incubated at 42 ° C. and 1000 rpm for 5 hours, and an ester exchange reaction between oil and methanol was performed. Lipids were extracted from the obtained samples, and fatty acid methyl esters were measured. The measurement results are shown in FIG. At methanol addition concentrations up to 30%, the yield of fatty acid methyl ester production increased with increasing addition concentrations. On the other hand, in a high concentration methanol solution of 35% or more, the yield decreased as the concentration increased.

<Example 6> Examination of the time of the second stage reaction of the two stage reaction of algae The culture solution obtained in Example 1 was centrifuged, sterilized water was added to the precipitate, and a 1-fold suspension was prepared. . Adjust the pH of the suspension to 4.5 with 1N HCl solution, add 1 ml to a 1.5 ml Eppendorf tube, preincubate at 55 ° C for 5 min, incubate at 55 ° C, 1000 rpm, 20 min, then centrifuge. 200 μl of 30% methanol solution was added to the precipitate. Each sample was incubated at 42 ° C. and 1000 rpm for each time, and a transesterification reaction between fat and methanol was performed. Lipids were extracted from the obtained samples, and fatty acid methyl esters were measured. The measurement results are shown in FIG. Compared with the reaction time of 30 min, the yield of fatty acid methyl ester production increased gradually with the elapse of 60 min, 90 min, 120 min, and 240 min. On the other hand, at the reaction temperature after 360 min, the yield tended to decrease gradually as the reaction time passed.

<Example 7> Examination of the temperature of the second stage reaction of the two stage reaction of algae The culture solution obtained in Example 1 was centrifuged, and sterilized water was added to the precipitate to prepare a 1-fold suspension. . After adjusting the pH of the suspension to 4.5 with 1N HCl solution, 1 ml was placed in a 1.5 ml Eppendorf tube and pre-incubated for 5 minutes by standing at 55 ° C. Next, each sample was incubated at 55 ° C, 1000rpm, 20min, then centrifuged, 200μl of 30% methanol solution was added to the precipitate, and incubated at 1000rpm for 2hr at each temperature, and the transesterification of oil and methanol Reaction was performed. Lipids were extracted from the obtained samples, and fatty acid methyl esters were measured. The measurement results are shown in FIG. Production of fatty acid esters was confirmed even at a reaction temperature of 5 ° C., and the yield of fatty acid esters increased to a reaction temperature of 35 ° C. as the temperature increased. On the other hand, at a reaction temperature of 40 ° C. or higher, the yield tended to decrease with increasing temperature.

<Example 8> Examination of added alcohol in two-stage reaction of algae The culture solution obtained in Example 1 was centrifuged, and sterilized water was added to the precipitate to prepare a 1-fold suspension. Adjust the pH of the suspension to 4.5 with 1N HCl solution, add 1 ml to a 1.5 ml Eppendorf tube, preincubate at 55 ° C for 5 min, incubate at 55 ° C, 1000 rpm, 20 min, then centrifuge. 200 μl of 10% methanol, 10% ethanol or 10% butanol solution was added to the precipitate. Each sample was incubated at 42 ° C., 1000 rpm, for 5 hours, and an ester exchange reaction between fat and alcohol was performed. Lipids were extracted from the obtained samples, and fatty acid alcohol esters were measured. The measurement results are shown in FIG. Compared to the case where 10% methanol was added, almost the same yield was confirmed even when 10% ethanol was added. Further, as in the case of adding methanol and ethanol, a plurality of fatty acid butanol ester bands were confirmed by the addition of butanol.

<Example 9> Qualitative analysis of fatty acid alcohol ester produced by two-step reaction The culture solution obtained in Example 1 was centrifuged, and sterilized water was added to the precipitate to prepare a 1-fold suspension. Adjust the pH of the suspension to 4.5 with 1N HCl solution, add 1 ml to a 1.5 ml Eppendorf tube, preincubate at 55 ° C for 5 min, incubate at 55 ° C, 1000 rpm, 20 min, then centrifuge. Then, 200 μl of 10% methanol / 10% ethanol solution was added to the precipitate. Each sample was incubated at 42 ° C., 1000 rpm, for 5 hours, and an ester exchange reaction between fat and alcohol was performed. Lipids were extracted from the obtained samples to qualify fatty acid alcohol esters. The results are shown in FIG. Almost the same fatty acid alcohol ester composition was shown in the experimental section of methanol and ethanol addition. However, myristic acid ethyl ester with ethanol addition has not been analyzed (denoted NA). The content of α-linolenic acid alcohol ester was the highest, and in addition, myristic acid methyl ester, palmitic acid alcohol ester, linoleic acid alcohol ester, oleic acid alcohol ester and stearic acid alcohol ester were confirmed.

<Example 10> Cultivation of Scenedesmus abundans UTEX 1358 strain Scenedesmus abundans UTEX 1358 strain was cultivated in a 500 mL Erlenmeyer flask containing 100 mL of Modified Bold 3N medium under sunshine conditions of 30 ° C and light intensity of 7,000 lux (light and dark for 11 hr each). Gradient method), while culturing for 7 days while maintaining the CO ₂ concentration in the incubator at 1%, this was used as a preculture solution. Note that white light from a fluorescent lamp was used as the light source. To a 500 mL Erlenmeyer flask containing 100 mL of Modified Bold 3N medium, 5 mL of the preculture solution was added and cultured under the same conditions for 16 days.

(Modified Bold 3N medium)
NaNO ₃ 750 mg / L
MgSO ₄・ 7H ₂ O 75 mg / L
KH ₂ PO ₄ 175 mg / L
K ₂ HPO ₄ 75 mg / L
CaCl ₂・ 2H ₂ O 25 mg / L
NaCl 25 mg / L
Na ₂ EDTA ・ 2H ₂ O 4.5 mg / L
FeCl ₃・ 6H ₂ O 0.582 mg / L
MnCl ₂・ 4H ₂ O 0.246 mg / L
ZnCl ₂ 0.03 mg / L
CoCl ₂・ 6H ₂ O 0.012 mg / L
Na ₂ MoO ₄・ 2H ₂ O 0.024 mg / L
HEPES 0.036 mg / L
Thiamine 1.1 mg / L
Biotin 0.025 mg / L
VitaminB ₁₂ 0.12 mg / L
CaCO ₃ 0.2 mg / L
Green house soil 0.2 tsp / L
After adjusting to pH 6.2, autoclave sterilization at 120 ° C for 15 minutes

<Example 11> Two-step reaction with Scenedesmus abundans UTEX 1358 strain The 100 ml culture solution obtained in Example 10 was centrifuged, and sterile water was added to the precipitate to prepare a 1-fold cell suspension. Adjust the pH of the suspension to 4.2 with 1N HCl solution, add 1 ml to a 1.5 ml Eppendorf tube, preincubate at 55 ° C for 5 min, incubate at 55 ° C, 1000 rpm, 20 min, then centrifuge. 200 μl of 20% methanol solution was added to the precipitate. It was incubated at 42 ° C. and 1000 rpm for 6 hours to carry out a transesterification reaction between fat and alcohol. Lipids were extracted from the obtained samples, and fatty acid methyl esters were measured. The results are shown in FIG. Production of fatty acid methyl esters was also confirmed in Scenedesmus abundans UTEX 1358 strain.

The fatty acid ester can be produced efficiently by the present invention.

Claims

(A) reacting a culture obtained by culturing microalgae in a medium at medium temperature;
(B) Then, an alcohol is added and reacted at a temperature lower than the intermediate temperature,
(C) A method for producing a fatty acid ester, wherein the fatty acid ester is collected from the reaction product obtained.
The method according to claim 1, wherein the temperature of the reaction (a) is 40 ° C or higher.
The method according to claim 1 or 2, wherein the temperature of the reaction (a) is 70 ° C or lower.
The method according to any one of claims 1 to 3, wherein the pH of the reaction (a) is from weakly acidic to weakly alkaline.
The method according to any one of claims 1 to 4, wherein the temperature of the reaction (b) is 5 ° C or higher.
The method according to any one of claims 1 to 5, wherein the temperature of the reaction (b) is 60 ° C or lower.
The method according to any one of claims 1 to 6, wherein the alcohol concentration in the reaction (b) is 5% or more.
The method according to any one of claims 1 to 7, wherein the alcohol concentration in the reaction (b) is 70% or less.
The method according to any one of claims 1 to 8, wherein the alcohol added to the reaction (b) is a lower alcohol having 5 or less carbon atoms.
The method according to any one of claims 1 to 8, wherein the alcohol added to the reaction (b) is a higher alcohol having 6 or more carbon atoms.
The method according to any one of claims 1 to 10, wherein the fatty acid ester is extracted by further treating with an organic solvent after the two-step reaction of (a) and (b), and the fatty acid ester is collected from the extract. .
The method according to claim 11, wherein the precipitate separated by centrifugation after the two-stage reaction is treated with an organic solvent.
The organic solvent treatment is performed in methanol, ethanol, 2-propanol, acetone, butanol, pentanol, hexanol, heptanol, octanol, chloroform, methyl acetate, ethyl acetate, dimethyl ether, diethyl ether, or hexane. The method described in 1.
The method according to any one of claims 1 to 13, wherein the microalgae are algae belonging to the green plant gate.
The method according to claim 14, wherein the microalgae are algae belonging to the class of green algae, treboxya algae, or plastinophyceae.
The method according to claim 15, wherein the microalgae are algae belonging to the green alga class.